中国科学院机构知识库网格
Chinese Academy of Sciences Institutional Repositories Grid
Two distinctive variational regions of radial particle concentration profiles in circulating fluidized bed risers

文献类型:期刊论文

作者Xu, GG; Sun, GG; Nomura, K; Li, JH; Kato, K
刊名POWDER TECHNOLOGY
出版日期1999-01-04
卷号101期号:1页码:91-100
ISSN号0032-5910
关键词circulating fluidized beds radial distribution hydrodynamics particle concentration modeling regime transition
其他题名Powder Technol.
中文摘要The radial profiles of particle concentration in circulating fluidized bed (CFB) risers experience actually a sequential variation as 'uniform (dense)-nonuniform-uniform (dilute), in response to the flow evolution from minimum fluidization to pneumatic transport. Through measuring the lateral distributions of solid concentration in the range epsilon(mf) similar to 1.0 of the cross-sectionally averaged voidage, it was found that the first variational stage, from dense uniform (minimum fluidization) to nonuniform, is completed via the rapid decrease of the particle concentration in the bed core, and the succeeding second stage, from nonuniform to dilute uniform (pneumatic transport), is implemented via the quick decrease of the particle concentration near the bed wall. Based on this observation, general correlations were proposed to predict the local voidages on the bed wall (specifically, at the point where the dimensionless radius is equal to 0.99) and at the bed center, which can be used for the entire spectrum of gas-solid fluidization regimes prevailing in CFB risers. Further analyses demonstrated that such two variational regions are related also to the regime transition and the lateral distribution features of the transient solid concentration fluctuations. (C) 1999 Elsevier Science S.A. All rights reserved.
英文摘要The radial profiles of particle concentration in circulating fluidized bed (CFB) risers experience actually a sequential variation as 'uniform (dense)-nonuniform-uniform (dilute), in response to the flow evolution from minimum fluidization to pneumatic transport. Through measuring the lateral distributions of solid concentration in the range epsilon(mf) similar to 1.0 of the cross-sectionally averaged voidage, it was found that the first variational stage, from dense uniform (minimum fluidization) to nonuniform, is completed via the rapid decrease of the particle concentration in the bed core, and the succeeding second stage, from nonuniform to dilute uniform (pneumatic transport), is implemented via the quick decrease of the particle concentration near the bed wall. Based on this observation, general correlations were proposed to predict the local voidages on the bed wall (specifically, at the point where the dimensionless radius is equal to 0.99) and at the bed center, which can be used for the entire spectrum of gas-solid fluidization regimes prevailing in CFB risers. Further analyses demonstrated that such two variational regions are related also to the regime transition and the lateral distribution features of the transient solid concentration fluctuations. (C) 1999 Elsevier Science S.A. All rights reserved.
WOS标题词Science & Technology ; Technology
类目[WOS]Engineering, Chemical
研究领域[WOS]Engineering
关键词[WOS]HEAT-TRANSFER ; GAS ; FLOW ; TURBULENT ; PRESSURE ; FLUCTUATIONS ; BEHAVIOR ; REGIMES
收录类别SCI
原文出处://WOS:000077805500010
语种英语
WOS记录号WOS:000077805500010
公开日期2013-11-15
版本出版稿
源URL[http://ir.ipe.ac.cn/handle/122111/6099]  
专题过程工程研究所_研究所(批量导入)
作者单位1.Gunma Univ, Dept Biol & Chem Engn, Kiryu, Gumma 376, Japan
2.Acad Sinica, Inst Chem Met, Beijing 100080, Peoples R China
推荐引用方式
GB/T 7714
Xu, GG,Sun, GG,Nomura, K,et al. Two distinctive variational regions of radial particle concentration profiles in circulating fluidized bed risers[J]. POWDER TECHNOLOGY,1999,101(1):91-100.
APA Xu, GG,Sun, GG,Nomura, K,Li, JH,&Kato, K.(1999).Two distinctive variational regions of radial particle concentration profiles in circulating fluidized bed risers.POWDER TECHNOLOGY,101(1),91-100.
MLA Xu, GG,et al."Two distinctive variational regions of radial particle concentration profiles in circulating fluidized bed risers".POWDER TECHNOLOGY 101.1(1999):91-100.

入库方式: OAI收割

来源:过程工程研究所

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